Mathematical Description of the Process of Impact Interaction of a Flow of Catalyst Particles with a Breaking Element in a Cyclone Device with a Coaxial Arrangement of Purification Stages

IF 0.6 4区 工程技术 Q4 ENGINEERING, CHEMICAL Theoretical Foundations of Chemical Engineering Pub Date : 2024-12-03 DOI:10.1134/S0040579524601237
A. E. Lebedev, M. A. Yurovskaya, I. S. Gudanov, V. K. Leontiev
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Abstract

Processes for cleaning solid particles from gases are used in many modern enterprises. Among the main requirements for gas-cleaning equipment are high purification degree, small overall dimensions, low hydraulic resistance, and ease of maintenance. All these requirements are met by a cyclone apparatus with a coaxial arrangement of cleaning stages, developed at Yaroslavl State Technical University. In this apparatus, three stages of purification of the dust and gas flow are arranged sequentially. At the first and third stages, the separation of solid particles from the gas flow occurs due to centrifugal force, and at the second stage, inertial settling of particles is effectuated. In addition, the first stage of the apparatus is equipped with a baffle element, which not only increases the efficiency of solid-phase separation, but also makes it possible to destroy the formed agglomerates due to the organization of impact interaction. The processes of centrifugal and inertial separation, implemented at the second and third stages of the apparatus, are currently studied almost completely, whereas the impact interaction of the particle flow with the baffle element remains poorly understood. In this paper, on the basis of a probabilistic approach, expressions are obtained for the differential distribution function of the number of particles of the solid phase captured by the centrifugal-impact stage of the cyclone apparatus with a coaxial arrangement of purification stages. Experimental studies have confirmed the adequacy of the formulated expressions for the average particle size. Thus, the obtained expressions for the differential distribution function of the number of particles make it possible to estimate the composition of the solid phase separated at the first stage and carried away with the gas flow to the second and third, which is necessary when drawing up an engineering method for calculating the apparatus.

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同轴排列净化级的旋风分离器中催化剂颗粒流与破碎元件的撞击相互作用过程的数学描述
许多现代企业都采用从气体中清除固体颗粒的工艺。对气体净化设备的主要要求是净化程度高、整体尺寸小、水力阻力小、维修方便。雅罗斯拉夫尔国立技术大学开发的同轴清洗级旋风装置可以满足所有这些要求。在该装置中,粉尘和气流的三个净化阶段按顺序排列。在第一和第三阶段,由于离心力,固体颗粒从气流中分离出来,在第二阶段,颗粒的惯性沉降实现。此外,该装置的第一级设有挡板元件,不仅提高了固相分离的效率,而且由于冲击相互作用的组织,使得形成的团聚体有可能被破坏。离心和惯性分离的过程,在装置的第二和第三阶段实施,目前几乎完全研究,而颗粒流与挡板元件的冲击相互作用仍然知之甚少。本文基于概率方法,得到了同轴布置的旋流器离心冲击级所捕获的固相颗粒数的微分分布函数表达式。实验研究证实了所建立的平均粒径表达式的充分性。由此得到的颗粒数的微分分布函数表达式,可以估计出在第一级分离并随气流进入第二级和第三级的固相的组成,这在制定计算仪器的工程方法时是必要的。
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来源期刊
CiteScore
1.20
自引率
25.00%
发文量
70
审稿时长
24 months
期刊介绍: Theoretical Foundations of Chemical Engineering is a comprehensive journal covering all aspects of theoretical and applied research in chemical engineering, including transport phenomena; surface phenomena; processes of mixture separation; theory and methods of chemical reactor design; combined processes and multifunctional reactors; hydromechanic, thermal, diffusion, and chemical processes and apparatus, membrane processes and reactors; biotechnology; dispersed systems; nanotechnologies; process intensification; information modeling and analysis; energy- and resource-saving processes; environmentally clean processes and technologies.
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